Quenching Medium Delivery in Hydroprocessing Catalyst Beds

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Solution Overview

Problem

Existing temperature control methods in hydroprocessing reactor vessels fail to achieve uniform temperature distribution across catalyst beds, leading to hot spots, inefficient catalyst use, and potential 'runaway' conditions due to inadequate mixing, non-uniform distribution, and catalyst wear.

Innovation Solution

Implementing a system with multipoint temperature sensing devices and selectively controlled quench pipes to independently manage temperature in various regions of the catalyst bed, allowing for real-time adjustments based on temperature profiles to maintain optimal reactivity levels.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If a single distribution tray is used to distribute reactants across the catalyst bed, then the device complexity is reduced, but the temperature distribution uniformity deteriorates leading to hot spots and inefficient catalyst utilization

Engineering Contradiction:
Improvedistribution system complexityVSAvoidtemperature distribution uniformity
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The single distribution tray is segmented into multiple independently controlled distribution zones, each capable of adjusting reactant flow to specific regions of the catalyst bed. This segmentation allows targeted temperature control in different bed regions without requiring a completely complex distributed system, thus resolving the contradiction between device simplicity and temperature uniformity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The distribution system provides locally adapted reactant distribution by adjusting flow rates to specific zones based on their temperature requirements. Each distribution zone can be optimized for its local conditions, addressing hot spots or cold regions selectively, thereby achieving uniform temperature distribution without uniformly complicating the entire system.

Inventive Principle:
Principle #3Local quality

2Temperature

If quench zones are provided above each catalyst bed for temperature control, then the temperature control capability is improved, but the device complexity increases due to multiple mixing devices and distribution trays

Engineering Contradiction:
Improvetemperature control capabilityVSAvoidmixing and distribution system complexity
Core Design Contradiction:
TemperatureVSDevice complexity

Solution Approach 1:

The distribution tray is designed to perform multiple functions: it distributes reactants uniformly across the catalyst bed, provides localized temperature control through zone-specific flow adjustment, and eliminates the need for separate quench zones above each bed. This multi-functionality reduces overall device complexity while maintaining temperature control capability.

Inventive Principle:
Principle #6Universality (Multi-functionality)

Solution Approach 2:

The quenching function and distribution function are merged into a single integrated system. The distribution tray incorporates quenching capability by injecting cooler hydrogen directly at the distribution points, eliminating the need for separate quench zones and mixing devices, thus reducing device complexity while preserving temperature control.

Inventive Principle:
Principle #5Merging (Combining)

3Device complexity

If inadequate mixing of hydrocarbon feed with hydrogen gas occurs, then the device complexity is reduced, but temperature uniformity deteriorates resulting in hot spots and unsafe operating conditions

Engineering Contradiction:
Improvemixing system complexityVSAvoidtemperature distribution uniformity
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

Hydrogen gas is pre-mixed with hydrocarbon feed in controlled ratios before entering the catalyst bed through the distribution tray. This preliminary mixing ensures uniform saturation of the feed stream with hydrogen, preventing hot spots caused by inadequate mixing without requiring complex in-bed mixing devices.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The distribution tray acts as an intermediary mixing zone where hydrogen and hydrocarbon feed are combined before contacting the catalyst. This intermediate mixing step ensures uniform reactant composition throughout the bed, preventing temperature non-uniformity while avoiding the need for complex direct-injection mixing systems within the catalyst bed.

Inventive Principle:
Principle #24Intermediary (Mediator)

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach enhances product yield, extends catalyst life, and prevents dangerous operating conditions by ensuring uniform temperature distribution and tailored reactivity across the catalyst bed.

Implementation Method 1

mixing the hot hydrocarbon liquid feed stream with a cooler stream of hydrogen gas

Methodology Applied
Scientific EffectMixing:

Implementation Method 2

mixing the hot hydrocarbon liquid feed stream with a cooler stream of hydrogen gas that is provided from an external source

Methodology Applied
Scientific EffectHeat transfer: Convection

Implementation Method 3

reacting the hydrocarbon material with hydrogen in a series of catalyst beds

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 4

because the hydroprocess is exothermic, a temperature profile of the bed generally should indicate an increase in temperature from the top to the bottom of the bed

Methodology Applied
Scientific EffectExothermic reaction: Exothermic Reaction

Data Source

PatentUS9617483B2Controlling temperature within a catalyst bed in a reactor vessel
Publication Date: 2017.04.11 DAILY JEFFREY N
  • US9617483B2 patent drawing
  • US9617483B2 patent drawing
  • US9617483B2 patent drawing

AI summary

A quenching medium is delivered directly to selected regions or locations within a catalyst bed in a hydroprocessing reactor vessel in order to control the reactivity of a hydroprocess occurring in the selected regions or locations separately from other regions or locations. Temperature sensors for providing temperature indications and conduits for delivering the quench medium are distributed throughout the catalyst bed. One or more conduits can be selected for delivery of the quenching medium to selected regions or locations so that separate control of the level of reactivity in each of various regions or locations throughout the bed can be achieved.